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This report presents a cost analysis of para-Xylene production from glucose syrup. The process examined is similar to the one proposed by the Catalysis Center for Energy Innovation (CCEI). In this process, glucose is converted to dimethylfuran (DMF), which is then reacted with ethylene to form para-Xylene. This report was developed based essentially on the following reference(s): Williams, C.L., "Cycloaddition of Biomass-Derived Furans for Catalytic Production of Renewable p-Xylene", University of Massachusetts, 2012. Keywords: Dextrose, Corn Starch, CCEI-PX, C8 Aromatics
This report presents a cost analysis of para-Xylene production from glucose syrup. The process examined is similar to the one proposed by GEVO. In this process, first, isobutanol is produced via glucose fermentation. Then, isobutanol is converted to para-Xylene through dehydration, oligomerization, and dehydrocyclization reactions. This report was developed based essentially on the following reference(s): (1) US Patent 8614077 issued to GEVO in 2013 (2) US Patent 20110087000, also issued to GEVO in 2011 Keywords: Dextrose, Corn Starch, C8 Aromatics, Dimerization, Bio-Based p-Xylene
This report presents a cost analysis of para-Xylene production from raw sugar. In this process, raw sugar (sucrose) is hydrolyzed into glucose and fructose, which are converted to sorbitol. Sorbitol is then condensed forming p-Xylene. Benzene is generated as by-product. This report was developed based essentially on the following reference(s): Keywords: C8 Aromatics, BTX, Condensation, Transalkylation, Hydrolysis, Sugar Inversion
This report presents a cost analysis of bio-based 1,3-Butadiene (BD) production from glucose syrup using a direct fermentation process. In this process, a 70 wt% glucose-water syrup is used as raw material in an anaerobic fermentation step for Butadiene production. This report was developed based essentially on the following reference(s): Keywords: BD, Dextrose, Glucose Fermentation, Anaerobic Fermentation, Sugarcane, Corn, Green Butadiene, Renewable Feedstock
This report presents a cost analysis of 1,3-Propanediol (PDO) production from glucose syrup using a fermentation process. The process examined is similar to DuPont process. In this process, a 70 wt% glucose-water syrup is used as raw material. This report was developed based essentially on the following reference(s): (1) US Patent 7745184, issued to DuPont and Genencor in 2010 (2) US Patent 6479716, issued to Archer-Daniels-Midland in 2002 Keywords: Bio-PDO, Trimethylene Glycol, Polytrimethylene Terephthalate, PTT, Aerobic Fermentation, Tate and Lyle
This report presents a cost analysis of bio-based 1,3-Butadiene (BD) production from raw sugar using a fermentation process. The process examined is similar to Global Bioenergies process. In this process, raw sugar (sucrose) is diluted and hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fed to an anaerobic fermentation step to produce 1,3-Butadiene. This report was developed based essentially on the following reference(s): Keywords: BD, Hydrolysis, Sugar Inversion, Dextrose, Glucose Fermentation, Anaerobic Fermentation, Green Butadiene, Renewable Feedstock
This report presents a cost analysis of bio-based 1,3-Butadiene (BD) production from glucose syrup using a direct fermentation process The process examined is similar to Global Bioenergies process. In this process, a 70 wt% glucose-water syrup is used as raw material in an aerobic fermentation step for Butadiene production. This report was developed based essentially on the following reference(s): (1) WO Patent 2014086781, issued to Global Bioenergies in 2014 (2) WO Patent 2014086780 issued to Global Bioenergies in 2014 Keywords: BD, Dextrose, Glucose Fermentation, Aerobic Fermentation, Sugarcane, Corn, Green Butadiene, Renewable Feedstock